JPS59184295A - Solid fuel and its preparation - Google Patents
Solid fuel and its preparationInfo
- Publication number
- JPS59184295A JPS59184295A JP5798983A JP5798983A JPS59184295A JP S59184295 A JPS59184295 A JP S59184295A JP 5798983 A JP5798983 A JP 5798983A JP 5798983 A JP5798983 A JP 5798983A JP S59184295 A JPS59184295 A JP S59184295A
- Authority
- JP
- Japan
- Prior art keywords
- coke
- oil
- solid fuel
- mixer
- sludge
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Description
【発明の詳細な説明】
本発明はo 7−スラッジ、スクリーンカス、及び廃
タイヤを蒸して得たコークス及び油を主原料とする固形
燃料及びその製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a solid fuel whose main raw materials are coke and oil obtained by steaming O7-sludge, screen scum, and waste tires, and a method for producing the same.
従来、尻タイヤを活用した固形燃料には、廃タイヤを焼
却することによって得られるカーボンブラックと灰を主
原料とし、これにリグニンを含んだノξルゾ廃液を粘結
剤として混合して練り合わせ適宜の大きさに造粒したも
のがあった。Conventionally, solid fuel using tail tires uses carbon black and ash obtained by incinerating waste tires as the main raw materials, and mixes lignin-containing waste liquid as a binder and kneads the mixture as appropriate. There was one that was granulated to the size of .
しかしこれは、廃タイヤを焼却して得られたカー、]?
ンブラックと灰をパルプ廃液と混合し造粒したものであ
るため、燃焼カロリーが低く固形燃料として十分な発熱
が得られなかった。But this is a car obtained by incinerating waste tires.]?
Because it is made by mixing black and ash with pulp waste liquid and granulating it, its combustion calorie is low and it cannot generate enough heat to be used as a solid fuel.
本発明は上記欠点に鑑みなされたもので、廃タイヤを圧
力釜で蒸して得たコークスと油を利用し、燃焼カロリー
が大きく低コストな同形燃料及びその製造方法を提供す
るものである。The present invention was made in view of the above-mentioned drawbacks, and it is an object of the present invention to provide a homogeneous fuel that burns a large amount of calories and is low in cost, and a method for producing the same, using coke and oil obtained by steaming waste tires in a pressure cooker.
このため本発明の目的を達成する固形燃料は15饅〜3
5チのペーパースラッジと、15チ〜35係のスクリー
ンカスと、69:4%〜25係のコークスと、0.3チ
以上の油と、15チ〜0.3%の松ヤニを含有してなる
。Therefore, the solid fuel that achieves the purpose of the present invention is 15 to 3
Contains 5 parts paper sludge, 15 parts to 35 parts screen scum, 69:4% to 25 parts coke, 0.3 parts or more oil, and 15 parts to 0.3% pine tar. It becomes.
又、その製造方法の第1は15チ〜35%のペーパース
ラッジと、15条〜35チのスクリーンカスを混合機で
混合し、しかる後、乾燥炉で乾燥させて乾燥物を得、こ
れに廃タイヤを圧力1だで蒸して得たコークスを粉状に
した粉状物69.4%〜25係及び油0.3%以上、さ
らには15%〜0.3チの松ヤニを混合機で混合して混
合物を得、これを押出し成形機で一定の形状に固結又は
破#1機で破細し微粉炭としたものである。The first manufacturing method is to mix 15 to 35% paper sludge and 15 to 35 pieces of screen sludge in a mixer, and then dry it in a drying oven to obtain a dry product. Mixing machine with 69.4% to 25% coke powder obtained by steaming waste tires at 1 pressure, 0.3% oil or more, and 15% to 0.3% pine tar. A mixture is obtained by mixing in a machine, and this is solidified into a certain shape with an extruder or crushed with a crusher #1 to obtain pulverized coal.
又、製造方法の第2は15%〜35%のべ一ノξ−スラ
ッジと、15%〜35係のスクリーンカスを混合機で混
合したものと、廃タイヤを圧力釜で蒸して得たコークス
を粉状にした粉状物69.4 %〜25%及び油0,3
%以上を混合機で混合したものの双方を乾燥PK入れて
乾燥し、この乾燥したものに15多〜0.3係の松ヤニ
を混合機で混合して混合物を得、これを押出し成形機で
一定の形状に固結又は破細機で破細し微粉炭としたもの
である。The second production method is to mix 15% to 35% of Beichino ξ-sludge, 15% to 35% of screen scum in a mixer, and coke obtained by steaming waste tires in a pressure cooker. Powdered material 69.4% to 25% and oil 0.3%
% or more in a mixer, add dry PK to the mixture, dry it, mix 15% to 0.3% pine resin in a mixer to obtain a mixture, and extrude this into an extruder. It is made into pulverized coal by solidifying it into a certain shape or crushing it with a crusher.
以下、本発明の一実施例を図面及び表を用いて説明する
。Hereinafter, one embodiment of the present invention will be described using drawings and tables.
iu、ペーノぞ−スラッジ、スクリーンカス、コークス
、油、松ヤニを用いた。固形燃料の例である。iu, penozo - sludge, screen scum, coke, oil, and pine resin were used. This is an example of solid fuel.
ペーパースラッジは製紙工場から生成されるもので水分
50%〜95%、好ましくa水分65チ〜80%を含有
するものを直接原料とするが、これを水分8チ〜30チ
好ましくは水分10チ〜20俤に乾燥したものを用いる
。又、スクリーンカスは段&−ル等の残渣叉はポリプロ
ピレン系の古紙の残渣である。Paper sludge is produced directly from paper mills and contains 50% to 95% moisture, preferably 65% to 80% moisture, but this is mixed with 8% to 30% water, preferably 10% moisture. Use dried to ~20 yen. Further, the screen residue is the residue of corrugated plates or the like, or the residue of polypropylene waste paper.
コークス及び油は廃タイヤを圧力釜で蒸した際に得られ
たものである。圧力釜を蒸す温度は1500’0〜23
00℃で好ましくは1700’0〜2o00°0である
。尚、廃タイヤを蒸した際に得られるピアノ線は除去す
る。又、コークスはこれを粉砕機で粉砕し粉状物にした
ものを用いる。松ヤニは凝固剤として用いるものである
。Coke and oil are obtained when waste tires are steamed in a pressure cooker. The temperature for steaming a pressure cooker is 1500'0~23
At 00°C, it is preferably 1700'0 to 2o00°0. Note that the piano wire obtained when steaming waste tires is removed. Further, the coke used is one that is crushed into powder using a crusher. Pine tar is used as a coagulant.
表において試料1 、2.10.17は本発明の適用範
囲以外の試料例を示し、試料■〜■、@〜〔ね本発明の
好ましい固形燃料を示す。In the table, samples 1, 2, 10, and 17 indicate sample examples outside the scope of the present invention, and samples ① to ① and @ to ① indicate preferred solid fuels of the present invention.
試料1,2にはペー・ξ−スラッジ又はスクリーンカス
の一方が14優である例を示したが、本発明では15優
以上であることがこの種間形燃料の有効活用上望ましい
。Samples 1 and 2 show examples in which either the P/ξ-sludge or the screen scum has a rating of 14. However, in the present invention, it is desirable to have a rating of 15 or more for effective use of this interspecies fuel.
又、試料17の如くペーパースラッジが35チヲ越える
と燃焼後の灰の量が多すきて固形燃料としては不向きで
ある。Moreover, if the paper sludge exceeds 35 inches as in Sample 17, the amount of ash after combustion will be large, making it unsuitable as a solid fuel.
これに対し試料■〜■+ o−0煎燃焼カロリーも45
00 kcaffl/kg−9500kcaffl/k
g <らいまで祷られるため一般的なこの種の固形燃料
としては好ましいものである。On the other hand, the calories burned for sample ■~■+o-0 were also 45
00kcaffl/kg-9500kcaffl/k
It is preferable as a general solid fuel of this type because it can be prayed for until leprosy.
尚、スクリーンカスはベー/e−スラッジの分量と同じ
<15%〜35%であることが望ましく15%未満では
燃焼カロリーが低すき35%を越えるものは収集が困難
なためこの種の固形シ;λ料としで(dふされしくない
。In addition, it is desirable that the amount of screen dregs is the same as the amount of base/e-sludge, <15% to 35%. If it is less than 15%, the burned calories will be low, and if it exceeds 35%, it will be difficult to collect, so this type of solid sludge is ; λ charge and (d unbecoming).
又、コークスハ、ベーノぐ−スラッジ、スクリーンカス
、及び油、松ヤニの最低必要な量に鑑み上限(は69.
4チぐらいまでで、下限匝は25優以上であることがこ
の種の固形燃料としては効果11っである。In addition, the upper limit (69.0
Up to about 4 inches, and the lower limit is 25 or more, which is the 11th effect for this type of solid fuel.
次に油は0.3係〜材、7%ぐらいまでであるが、これ
はコークスの量との関係で最低でも0.3%以上必要な
もので、44.7条を越えろものはこの種の燃料として
は燃焼カロリーが高</!る。但し分z電か乙の際の釜
の栄件が菫えばこれに限定されない。Next, the oil content is 0.3% to 7%, but this is required at least 0.3% in relation to the amount of coke, and this kind of oil exceeds Article 44.7. Burns a lot of calories as a fuel! Ru. However, it is not limited to this if the performance of the kettle at the time of delivery is satisfactory.
叉、松ヤニは15饅〜0.3俤ぐらいまでであるが、0
.3%未満では固形燃料としての凝固が困難てあシ、形
層れやひび割れを生じ、15%をに1,5えるとコスト
薗となり好丑しくない。However, pine tar costs between 15 yen and 0.3 yen, but 0.
.. If it is less than 3%, it will be difficult to solidify as a solid fuel, resulting in cracks, deformation, and cracks, and if it exceeds 15%, it will increase the cost, which is not desirable.
次に本発明の固形燃料の製法について図面を参照して説
明する。Next, the method for manufacturing solid fuel of the present invention will be explained with reference to the drawings.
(1)第1の方法
同図において、廃タイヤ1は自M車その他の廃物を利用
したタイヤであり、これをコンベア2上を移動してホノ
・ξ−3を介して圧力釜4に収納する。圧力釜はバーナ
ー5にて加熱され1800℃の熱風にて蒸さイする。6
はコークスの取り出し口である。取り出されたコークス
は流状体又は冷却後固形にされたものを粉砕機7にて粉
砕し粉状物とする。8はオイルタンクで圧力釜4の下方
に取り付けられた油の取シ出し口から油を導き一時貯留
する。オイルタンク8の油は混合機13に原料として導
かれ又、一部はiイン−5の燃料、乾燥炉12を用いる
湯合はその燃料に供される。(1) First method In the figure, a waste tire 1 is a tire made from waste from own vehicle or other vehicles, and is moved on a conveyor 2 and stored in a pressure cooker 4 via a hono/ξ-3. do. The pressure cooker is heated with burner 5 and steamed with hot air at 1800°C. 6
is the coke outlet. The taken out coke is either in a fluid state or solidified after cooling, and is crushed by a crusher 7 into powder. Reference numeral 8 denotes an oil tank that introduces oil from an oil outlet installed below the pressure cooker 4 and temporarily stores it therein. The oil in the oil tank 8 is led to the mixer 13 as a raw material, and part of it is used as fuel for the i-in-5, and a part of the oil is used as fuel for the melting process using the drying oven 12.
ペーパ−スラッジ9は水分60%〜70係のものを用い
スクリーンカス10と共に混合機11にて入れられ混合
される。この混合機11で混合された混合物は次に乾燥
炉12で乾僅され水分10饅〜20チぐらいの混合物と
される。混合機13では粉砕(幾7で粉砕されたコーク
スと、オイルタンク8から導かれる油と、乾燥炉12で
乾燥されたペーパースラッジ及びスクリーンカスの乾燥
物と、松へ二14が入れられ混合される。Paper sludge 9 with a moisture content of 60% to 70% is put into a mixer 11 together with screen waste 10 and mixed. The mixture mixed in this mixer 11 is then dried in a drying oven 12 to form a mixture with a moisture content of about 10 to 20 cents. In the mixer 13, the coke pulverized in the pulverized step 7, the oil led from the oil tank 8, the paper sludge and screen scum dried in the drying oven 12, and the pine needle 14 are put and mixed. Ru.
尚、あらかじめ乾燥したペーパースラッジ9を用いると
きは、点線で示す如くとのに−・ぐ−スラツジ9及びス
クリーンカス10を混合機13に直接混入させてもよい
。In addition, when using the paper sludge 9 that has been dried in advance, the sludge 9 and the screen sludge 10 may be directly mixed into the mixer 13 as shown by the dotted line.
Jiff L出し成形機15はスクリュー型の11」シ
出し成形機でti、合4;Q、B1:3にで混合し得ら
れた混合物を押し出し成形し一定の大きさに裁断し固形
燃料16を得る。又、破細機18は混合機13からの混
合物を破細し微粉炭19を得るものである。The Jiff L extrusion molding machine 15 is a screw-type 11" extrusion molding machine that mixes ti, 4; obtain. Further, the crusher 18 crushes the mixture from the mixer 13 to obtain pulverized coal 19.
(2)第2の方法
第2の方法は第1の方法とほぼ同じであるが図において
、乾燥炉12に入れて乾燥するのはペー・ξ−スラッジ
9とスクリーンカス10を混合機11で混合したものと
、粉砕機7で粉砕されたコークス及びこれにオイルタン
ク8からのiil′f:混合機17にて混合したものの
双方を入れろものである。かくして得られた乾燥物を混
合機13にて松ヤニと混合したものを押出し成フ1刻残
で押出し成形叉は破細機で微粉炭とする。(2) Second method The second method is almost the same as the first method, but in the figure, the Pξ-sludge 9 and the screen sludge 10 are placed in the drying oven 12 and dried in the mixer 11. In this case, both the coke crushed by the crusher 7 and the coke from the oil tank 8 mixed in the mixer 17 are added. The thus obtained dried product is mixed with pine tar in a mixer 13, and the extrusion mixture is extruded into pulverized charcoal using a shredder.
尚、本う′ら明ば、基本的に1rまぺ−・?−スラッジ
とスクリーンカスに、B≦タイヤを蒸して得たコークス
と油を混合し、これに松ヤニを加えた混合物としこれを
押出し成形叉は微粉炭とした固形燃料である。この限り
において、ペーパ−スラッジ、スクリーンカス、コーク
ス、油、松ヤニをどの時点で加えるかはその他にも適宜
考えられるもので、上記二つの方法に限定されない。By the way, the main course is basically 1R page...? - It is a solid fuel in which sludge and screen residue are mixed with coke and oil obtained by steaming B≦ tires, and pine resin is added to this mixture, and this is extruded or made into pulverized coal. To this extent, the timing of adding paper sludge, screen scum, coke, oil, and pine tar may be considered at any other point and is not limited to the above two methods.
このように本発明の固形燃料はペー・ξ−スラッジと、
スクリーンカスに、〃タイヤを蒸して得られたコークス
とi市を混合し、これに十公ヤニを刀1jえたので次の
効果をイ]する。In this way, the solid fuel of the present invention includes P-ξ-sludge,
Mix the coke obtained by steaming the tires with the screen residue, and add 100 g of tar to it to create the following effect.
■、廃タイヤの処分に1]−1っていたものを有効な)
5′も料として再利用できる。■, Effective for disposing of waste tires (1]-1)
5' can also be reused as a material.
■、廃タイヤを蒸して得られたコークス及び油は単独で
燃焼させると8000 kcE4/J〜10(1)Ok
・コεンJの熱量が得られろためペーパースラッジ及び
スクリーンカスとの望ましい混合の割り・Gいによって
好ましい燃焼カロリーで低コストな固プレ燃料をイ石る
ことかできる。■Coke and oil obtained by steaming waste tires produce 8000 kcE4/J~10(1) Ok when burned alone.
・Since the calorific value of the cone J can be obtained, it is possible to produce a low-cost solid prefuel with a preferable combustion calorie depending on the desired mixing ratio with the paper sludge and screen scum.
図面は本発明の固形燃料の部活方法を示した説明図であ
る。The drawing is an explanatory view showing the solid fuel club activity method of the present invention.
Claims (2)
チ〜35チのスクリーンカスと、69.4%〜25チの
コークスと、’0.3%以上の油と、15%〜0.39
6の松ヤニを含有した固形燃料。(1), 15% to 35% P-ξ-sludge, and 15% to 35%
Screen scum of 1 to 35 t, coke of 69.4% to 25 t, oil of 0.3% or more, and 15% to 0.39
Solid fuel containing pine tar.
イヤを蒸して得たコークスと油を混合し、これに松ヤニ
を加えた混合物を得、これを押出し成形又は微粉炭とし
た固形燃料の製造方法。(2) Penozo - Mix coke and oil obtained by steaming waste tires with Penozo-Thranocytoscreen residue, add pine resin to this to obtain a mixture, and obtain a mixture that is extruded or made into pulverized coal as solid fuel. manufacturing method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5798983A JPS59184295A (en) | 1983-04-04 | 1983-04-04 | Solid fuel and its preparation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5798983A JPS59184295A (en) | 1983-04-04 | 1983-04-04 | Solid fuel and its preparation |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59184295A true JPS59184295A (en) | 1984-10-19 |
Family
ID=13071415
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5798983A Pending JPS59184295A (en) | 1983-04-04 | 1983-04-04 | Solid fuel and its preparation |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59184295A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20010069804A (en) * | 2001-05-12 | 2001-07-25 | 이광수 | Paper sludge fuel manufacturing plant and Method thereof |
KR100847511B1 (en) | 2007-05-17 | 2008-07-22 | 천명원 | Solid fuel and manufacturing method for the same |
JP2010194427A (en) * | 2009-02-24 | 2010-09-09 | Kitagawa Iron Works Co Ltd | Preservation method for high water content organic matter and solid fuel produced from the same |
JP2014205810A (en) * | 2013-04-16 | 2014-10-30 | 株式会社知多リサイクル | Solid fuel, and production method and device thereof |
RU2608733C1 (en) * | 2015-11-10 | 2017-01-23 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Кузбасский государственный технический университет имени Т.Ф. Горбачева" (КузГТУ) | Fuel briquette based on carbon residue of pyrolysis of tires |
JP2020111652A (en) * | 2019-01-10 | 2020-07-27 | 王子ホールディングス株式会社 | Solid fuel, manufacturing method of solid fuel and manufacturing apparatus of solid fuel |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56122896A (en) * | 1980-03-04 | 1981-09-26 | Meirin Denki Seisakusho:Kk | Production of solid fuel containing large quantity of organic industrial waste |
-
1983
- 1983-04-04 JP JP5798983A patent/JPS59184295A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56122896A (en) * | 1980-03-04 | 1981-09-26 | Meirin Denki Seisakusho:Kk | Production of solid fuel containing large quantity of organic industrial waste |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20010069804A (en) * | 2001-05-12 | 2001-07-25 | 이광수 | Paper sludge fuel manufacturing plant and Method thereof |
KR100847511B1 (en) | 2007-05-17 | 2008-07-22 | 천명원 | Solid fuel and manufacturing method for the same |
JP2010194427A (en) * | 2009-02-24 | 2010-09-09 | Kitagawa Iron Works Co Ltd | Preservation method for high water content organic matter and solid fuel produced from the same |
JP2014205810A (en) * | 2013-04-16 | 2014-10-30 | 株式会社知多リサイクル | Solid fuel, and production method and device thereof |
RU2608733C1 (en) * | 2015-11-10 | 2017-01-23 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Кузбасский государственный технический университет имени Т.Ф. Горбачева" (КузГТУ) | Fuel briquette based on carbon residue of pyrolysis of tires |
JP2020111652A (en) * | 2019-01-10 | 2020-07-27 | 王子ホールディングス株式会社 | Solid fuel, manufacturing method of solid fuel and manufacturing apparatus of solid fuel |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2502974A1 (en) | Densified fuel pellets | |
JP5777207B2 (en) | Method for producing carbide from fibrous biomass | |
KR20060096392A (en) | A solid fuel manufacturing method and its device use of the food waste and the plastic waste | |
JPH0987646A (en) | Production of solid fuel using organic waste | |
EP2090641B1 (en) | Densified fuel pellets | |
JPS59184295A (en) | Solid fuel and its preparation | |
JPS6128589A (en) | Method and apparatus for producing solid fuel | |
JP3205042B2 (en) | Method for producing solid fuel and solid fuel produced thereby | |
KR100297320B1 (en) | Automatic charcoal manufacturing system | |
JPH0631362B2 (en) | Method for producing solid fuel from solid organic waste | |
CN1039348C (en) | Process for manufacturing composite solid fuel from coal and vegetable material | |
CA1115955A (en) | Cellulosic material and thermoplastic polymer in fuel pellets | |
JPS58125790A (en) | Preparation of fuel from organic dust | |
CN1039346C (en) | Process for manufacturing composite solid fuel from coal and vegetable material | |
CN1064993C (en) | Compound coal and its manufacture technique | |
KR102584090B1 (en) | Manufacturing method of wood pellet using sawdust and waste powder paint as main materials | |
JPS59184294A (en) | Solid fuel and its preparation | |
JP2003201490A (en) | Method for producing solid fuel | |
KR100813616B1 (en) | The method for manufacturing and apparatus of solid fuel | |
JP2004285312A (en) | Fuel obtained by solidifying vegetable waste oil, and its manufacturing method | |
JP5084273B2 (en) | Method and apparatus for producing solid carbon fuel and plastic mixed solid fuel | |
JPS58189296A (en) | Production of solid fuel | |
KR20240021392A (en) | Manufacturing Method of Solid Fuel Using Waste Powdery Paint and Sawdust | |
JPS58152094A (en) | Composite solid fuel and its preparation | |
JPS6088093A (en) | Fuel pellet containing petroleum coke blended therewith |